This invention is directed to an improved process for preparing 2-phenylethylene phosphonic acid by reacting styrene and pcl5 in an inert organic solvent and hydrolyzing the reaction product formed, wherein the improvement comprises forming a mixture of styrene and pcl5 in a molar ratio of about 1:1 at a temperature of from 60° to 70° C. in an inert organic solvent having a boiling point above 70°C; maintaining the mixture at a temperature of from 60° to 70° C. with evolution of HCl gas until a clear solution forms; distilling off the solvent under vacuum; hydrolyzing the remaining reaction mixture in water at temperatures not exceeding 70°C and cooling the hydrolyzed mixture to cause crystals of 2-phenylethylene phosphonic acid to precipitate; and recovering said crystals.
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1. In a process for preparing 2-phenylethylene phosphonic acid by reacting styrene and pcl5 in an inert organic solvent and hydrolyzing the reaction product formed,
the improvement which comprises forming a mixture of styrene and pcl5 in a molar ratio of about 1:1 at a temperature of from 60° to 70°C in an inert organic solvent having a boiling point above 70°C; maintaining the mixture under agitation at a temperature of from 60° to 70°C with evolution of HCl gas until a clear solution forms; distilling off the solvent under vacuum; hydrolyzing the remaining reaction mixture in water at temperatures not exceeding 70°C and cooling the hydrolyzed mixture to cause crystals of 2-phenylene phosphonic acid to precipitate; and recovering said crystals.
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This invention is directed to the preparation of 2-phenylethylene phosphonic acid. More specifically, this invention is directed on improved method of preparing 2-phenylethylene phosphonic acid by reacting styrene with PCl5.
The reaction with styrene with twice the molar amount of PCl5 in the presence of an inert organic solvent such as benzene and the subsequent conversion into 2-phenylethylene phosphonic acid by hydrolysis is known. The pure acid is obtained with a total yield of approximately 34% subsequently to recrystallization from dibromomethane.
The preparation of 2-phenylethylene phosphonic acid by chlorination of a mixture of styrene and phosphorus trichloride and subsequent hydrolysis is also known. However, it is unavoidable during this reaction that a large amount of the added styrene escapes conversion into phosphonic acid due to the formation of chlorination products.
Finally, a continuous process has been disclosed in German Published Application (DE-OS) No. 23 43 460 in which 2-phenylethylene phosphonic acid is prepared by the reaction of styrene with twice the molar amount of PCl5 and subsequent hydrolysis, POCl3 being used as solvent. This process has the disadvantage that considerable amounts of PCl5 as well as POCl3 must be used.
It is an object of the invention to provide a method for the preparation of 2-phenylethylene phosphonic acid.
It is also an object of the invention to provide an improved method of preparing 2-phenylethylene phosphonic acid by reacting styrene and PCl5 in an inert organic solvent and hydrolyzing the reaction product formed, wherein the improvement comprises forming a mixture of styrene and PCl5 in a molar ratio of about 1:1 at a temperature of from 60° to 70°C in an inert organic solvent having a boiling point above 70°C; maintaining the mixture at a temperature of from 60° to 70°C with evolution of HCl gas until a clear solutions forms; distilling off the solvent under vacuum; hydrolyzing the remaining reaction mixture in water at temperatures not exceeding 70°C and cooling the hydrolyzed mixture to cause crystals of 2-phenylethylene phosphonic acid to precipitate; and recovering said crystals.
These and other objects of the invention will become more apparent from the discussion below.
It has been found that the presently known process of preparing 2-phenylethylene phosphonic acid can be improved. According to the improved method, styrene and PCl5 are mixed at a molar ratio of 1:1 and at temperatures of from about 60° to 70°C, in an inert organic solvent having a boiling point above 70°C, and the mixture is kept at this temperature under agitation with evolution of HCl gas until a clear solution is formed. The solvent is then removed under vacuum, the reaction product is transferred into water and hydrolyzed at a temperature not exceeding 70°C, and the product is crystallized from the subsequently cooled solution.
Suitable inert organic solvents for carrying out the process include, for example, benzene, toluene, chlorobenzene, xylene, and chlorinated hydrocarbons having a boiling point above 70°C Advantageously the organic solvent is used in an amount such that from about 300 to 600 ml of solvent are available per mol of PCl5.
When the stipulated conditions are observed, the process of the invention has the advantage that 2-phenylethylene phosphonic acid can be prepared with good yields and that only 1 mol of PCl5 is needed per mol of styrene.
The 2-phenylethylene phosphonic acid can be used with good effect as a collector for the recovery of stannic oxide by flotation.
The following example is intended to illustrate the invention and is not to be construed as limiting the invention thereto.
Amounts of 18.5 kg of toluene and 20.8 kg of PCl5 are placed in an enamelled agitator reactor and heated to 60°C under agitation. At this temperature, 10.4 kg of styrene dissolved in 18.5 kg of toluene are added, the addition being controlled in such a manner that the exothermic reaction keeps the reaction temperature between 60° and 70° C. The agitation is continued at this temperature until an almost clear solution is obtained. The reaction time is approximately 4 to 5 hours. The HCl gas evolved during this time is removed through an absorption tower.
The toluene is then distilled off under vacuum, while the pot temperature is kept from rising above 70°C The styryl phosphonic acid tetrachloride formed is transferred into 64 kg of water for the hydrolysis, while care is taken that the temperature does not exceed 70°C 2-Phenylethylene phosphonic acid precipitates from the cooled hydrolysis mixture in the form of a white crystalline product. It is filtered off and dried at 70°C The crude yield is 89 percent (based on styrene).
The preceding specific embodiments are illustrative of the practice of the invention. It is to be understood, however, that other expedients known to those skilled in the art or disclosed herein, may be employed without departing from the spirit of the invention or the scope of the appended claims.
| Patent | Priority | Assignee | Title |
| Patent | Priority | Assignee | Title |
| 2685602, | |||
| 3763122, | |||
| 3931294, | Sep 29 1973 | Hoechst Aktiengesellschaft | Production of 2-phenyl-ethylene phosphonic acid |
| DD76974, |
| Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
| Jan 28 1981 | MEFFERT, ALFRED | Henkel Kommanditgesellschaft auf Aktien | ASSIGNMENT OF ASSIGNORS INTEREST | 003920 | /0961 | |
| Jan 28 1981 | TESMANN, HOLGER | Henkel Kommanditgesellschaft auf Aktien | ASSIGNMENT OF ASSIGNORS INTEREST | 003920 | /0961 | |
| Mar 04 1981 | Henkel Kommanditgesellschaft auf Aktien | (assignment on the face of the patent) | / |
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